Liquid-liquid equilibria for systems of (water + carboxylic acid + methylcyclohexanol) at 293.15 K: Modeling considerations

Journal of Chemical and Engineering Data

Volumn 49, Issue 6, 2004, Pages 1815-1820

  Senol, Aynur ^a  

^a ISTANBUL UNIVERSITY   (Turkey)

Author keywords

[No Author keywords available]

Indexed keywords

ACETIC ACID; ACIDS; CATALYSIS; DIPOLE ANTENNAS; HYDROGEN BONDS; PARAMETER ESTIMATION; SOLUBILITY; VAPOR PRESSURE;

DIPOLE MOVEMENTS; POLAR COMPONENTS; PROPIONIC ACID; SOLVATION ENERGY;

PHASE EQUILIBRIA;

EID: 9744253059     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je0497606     Document Type: Article

References (22)

1. Arce, A.; Blanco, A.; Souza, P.; Vidai, I. Liquid-Liquid Equilibria of the Ternary System Water + Propanoic Acid + Methyl Isobutyl Ketone at Various Temperatures. J. Chem. Eng. Data 1993, 38, 201-203.
2. Letcher, T. M.; Redhi, G. G. Phase Equilibria for Mixtures of (Butanenitrile + a Carboxylic Acid + Water) at 298.15 K. Fluid Phase Equilib. 2002, 193, 123-133.
3. Darwish, N. A.; Abdulkarim, M. A.; Ashour, I.; Dwaidar, A. M.; Athamneh, F. S. Liquid-Liquid Equilibrium for the System Water + Acetic Acid + 1-Heptanol at 278.1, 293.1, 303.1 and 313.1 K. Fluid Phase Equilib. 2002, 200, 277-285.
4. Briones, J. A.; Mullins, J. C.; Thies, M. C. Liquid-Liquid Equilibria for the Oleic Acid-Beta-Sitosterol Water-System at Elevated-Temperatures and Pressures. Ind. Eng. Chem. Res. 1904, 33, 151-156.
5. Reinsel, M. A.; Borkowski, J. J. Partition Coefficients for Acetic, Propionic, and Butiric Acids in a Crude Oil/Water System. J. Chem. Eng. Data 1994, 39, 513-516.
6. Letcher, T. M.; Redhi, G. G. Phase Equilibria for Liquid Mixtures of (Benzonitrile + a Carboxylic Acid + Water) at T = 298.15 K. J. Chem. Thermodyn. 2001, 33, 1555-1565.
7. Aljimaz, A. S.; Fandary, M. S. H.; Alkandary, J. A.; Fahim, M. A. Liquid-Liquid Equilibria of the Ternary System Water + Acetic Acid + 1-Heptanol. J. Chem. Eng. Data 2000, 45, 301-303.
8. Colombo, A.; Battilana, P.; Ragaini, V.; Bianchi, C. L.; Carvoli, G. Liquid-Liquid Equilibria of the Ternary Systems Water + Acetic Acid + Ethyl Acetate and Water + Acetic Acid + Isophorone (3,5,5-Trimethyl-2-cyclohexen-1- one). J. Chem. Eng. Data 1999, 44, 35-39.
9. Wisniak, J.; Tamir, A. Liquid-Liquid Equilibrium and Extraction: A Literature Source Book; Elsevier: Amsterdam, 1980-1981.
10. Kamlet, M. J.; Doherty, R. M.; Abraham, M. H.; Marcus, Y.; Taft, R. W. Linear Solvation Energy Relationships. 46. An Improved Equation for Correlation and Prediction of Octanol/Water Partition Coefficients of Organic Nonelectrolytes (Including Strong Hydrogen Bond Donor Solutes). J. Phys. Chem. 1988, 92, 5244-5255.
11. Marcus, Y. Linear Solvation Energy Relationships: Correlation and Prediction of the Distribution of Organic Solutes between Water and Immiscible Organic Solvents. J. Phys. Chem. 1991, 95, 8886-8891.
12. Gmehling, J.; Li, J.; Schiller, M. Modified UNIFAC Model. 2, Present Parameter Matrix and Results for Different Thermodynamic Properties. Ind. Eng. Chem. Res. 1993, 32, 178-193.
13. Gmehling, J.; Rasmussen, P.; Fredenslund, Aa. Vapor-Liquid Equilibria by UNIFAC Group Contribution: Revision and Extension 2, Ind. Eng. Chem. Process Des. Dev. 1982, 21, 118-127.
14. Magnussen, T.; Rasmussen, P.; Fredenslund, Aa. UNIFAC Parameter Table for Prediction of Liquid-Liquid Equilibria. Ind. Eng. Chem. Process Des. Dev. 1981, 20, 331-339.
15. Senol, A.; Alptekin, G.; Sayar, A. A. Liquid-Liquid Equilibria of Some (Water + Tetrahydrofuran + Solvent) Ternaries at the Temperature (293.2 ± 0.1) K and Pressure (101.3 ± 0.7) kPa. J. Chem. Thermodyn. 1996, 27, 525-529.
16. Senol, A.; Sayar, A. A. Liquid-Liquid Equilibria of Some Water + Tetrahydrofurfuryl Alcohol + Solvent Ternaries at 293.2 ± 0.1 K and 101.3 ± 0.7 kPa. Fluid Phase Equilib. 1998, 106, 169-183.
17. Fredenslund, Aa.; Michelsen, M. L.; Sørensen, J. M. 2nd International Conference on Phase Equilibria and Fluid Properties; Berlin, March, 1980.
18. Taylor, R.; Koorjman, H. Composition Derivatives of Activity Coefficient Models (for the Estimation of Thermodynamic Factors in Diffusion). Chem. Eng. Commun. 1991, 102, 87-106.
19. Mori, H.; Oda, A.; Ito, C.; Aragaki, T.; Liu, F. Z. Thermodynamic Factors Derived from Group Contribution Activity Coefficient Models. J. Chem. Eng. Jpn. 1998, 29, 396-398.
20. Himmelblau, D. M. Basic Principles and Calculations in Chemical Engineering; Prentice Hall: Englewood Cliffs, NJ, 1989.
21. Barton, A. F. M. Solubility Parameters. Chem. Rev. 1975, 75, 731-753.
22. Riddick, J. A.; Bunger, W. B.; Sakano, T. K. Organic Solvents: Physical Properties and Methods of Purification; Wiley-Interscience: New York, 1986.